A cathode supply (30) for a fuel cell (10) of a fuel cell unit (1) for a fuel cell system is provided, the cathode supply (30) including a cathode supply path (31) and a cathode exhaust gas path (32) and at least two fluid pumping devices (33, 133) for pumping a cathode operating medium (5) for the fuel cell (10) are fluido-mechanically coupled into the cathode supply path (31), at least one first fluid pumping device (133) of the at least two fluid pumping devices (33, 133) being drivable only on the basis of an enthalpy in a cathode exhaust gas (6) of the fuel cell (10). A fuel cell unit for a vehicle, in particular, an electric vehicle, a fuel cell system for a vehicle, in particular, an electric vehicle, or a vehicle in particular an electric vehicle, the fuel cell unit, the fuel cell system, or the vehicle including a cathode supply (30) is provided.
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1. A cathode supply for a fuel cell of a fuel cell unit for a fuel cell system, the cathode supply comprising:
a cathode supply path;
a cathode exhaust gas path; and
at least two fluid pumps for pumping a cathode operating medium for the fuel cell being fluido-mechanically coupled into the cathode supply path;
at least one first fluid pump of the at least two fluid pumps being drivable by enthalpy in a cathode exhaust gas of the fuel cell.
2. The cathode supply as recited in
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5. The cathode supply as recited
6. The cathode supply as recited in
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10. The cathode supply as recited in
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12. The cathode supply as recited in
13. The cathode supply as recited in
14. The cathode supply as recited in
15. The cathode supply as recited in
16. The cathode supply as recited in
18. The fuel cell unit or system for a vehicle as recited in
21. The fuel cell unit as recited in
22. The fuel cell unit as recited in
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This claims the benefit of German Patent Application DE102015221597.0, filed Nov. 4, 2015 and hereby incorporated by reference herein.
The present invention relates to a cathode supply for a fuel cell of a fuel cell unit for a fuel cell system. Furthermore, the present invention relates to a fuel cell unit for a vehicle, a fuel cell system for a vehicle, and/or a vehicle, in particular, an electric vehicle.
A fuel cell of a fuel cell unit of a fuel cell system uses electrochemical conversion of a hydrogen-containing (H, H2) fuel to water, using oxygen (0, 02) to generate electrical energy. For this purpose, the fuel cell contains at least one so-called membrane electrode assembly (MEA) as a core component, which is a structure of an ion-conducting, or proton-conducting membrane and electrodes situated on both sides of the membrane, an anode electrode, and a cathode electrode. In addition, gas diffusion layers (GDL) may be situated on both sides of the membrane electrode assembly on the sides of the electrodes facing away from the membrane.
In general, the fuel cell is formed by a plurality of membrane electrode assemblies arranged in a stack, their electrical powers being combined during operation of the fuel cell. Bipolar plates, also known as flow field plates or separator plates, are usually situated between the individual membrane electrode assemblies, which ensure supply of operating media, known as reactants, to the membrane electrode assemblies, i.e., supply to the individual cells of the fuel cell, also usually serving as coolants. In addition, the bipolar plates ensure an electrically conductive electrical connection to the adjacent membrane electrode assemblies.
During operation of the individual cells of the fuel cell (individual cell: membrane electrode assembly and an associated anode space delimited by a bipolar plate and an associated cathode space delimited by a second bipolar plate), the fuel, a so-called anode operating medium, is fed to the anode electrodes via a flow field of the bipolar plate, open on the anode side, where an electrochemical oxidation of H2 to 2H+ takes place (H2=>2H++2e−) with the release of electrons (2e−). Water-bound or water-free transport of the formed protons (H+), from the anode electrodes ((complex) anode of the fuel cell), in the anode spaces of the individual cells to the cathode electrodes ((complex) cathode of the fuel cell) in the cathode spaces of the individual cells takes place through the membranes or electrolytes of the membrane electrode assemblies, which gas-tightly separate and electrically insulate the respective reaction spaces (anode space-cathode space pairs of the individual cells).
The electrons provided on the anode are conducted to the cathode via an electrical conductor and an electrical consumer (electric traction motor, AC unit, etc.). An oxygen-containing cathode operating medium is fed to the cathode electrodes of the cathode via a flow field of the bipolar plates open on the cathode side, a reduction from O2 to 2O2− taking place with the reception of electrons (½O2+2e−=>O2−). At the same time, the oxygen anions (O2−) formed at the cathode electrodes react with the protons transported through the membranes or electrolytes, with the formation of water (O2−+2H−=>H2O)
In order to supply a fuel cell stack, henceforth referred to mainly as fuel cell, with the operating media, the fuel cell has on the one hand, an anode supply and, on the other hand, a cathode supply. The anode supply has an anode supply path for feeding the anode operating medium into the anode spaces of the fuel cell and an anode exhaust gas path for removing an anode exhaust gas from the anode spaces. Similarly, the cathode supply has a cathode supply path for feeding the cathode operating medium into the cathode spaces of the fuel cell and a cathode exhaust gas path for removing a cathode exhaust gas from the cathode spaces.
For operating the fuel cell system, oxygen must be provided as cathode operating medium, mostly in the form of ambient air. Depending on the mode of operation of the fuel cell system, the air must be supplied compressed to a certain fluid pressure above the ambient air pressure (approximately 1 bar and less) and at a certain air mass flow rate. In particular, at comparatively high air masses and comparatively high fluid pressures, this is no longer feasible using a single one-stage fluid pumping device. In modern fuel cell units, an electrically driven turbocharger, known as electric turbocharger, is used. The electric turbocharger is the largest parasitic consumer in the fuel cell system.
Furthermore, the cathode exhaust gas of the fuel cell system has a certain energy content due to its temperature level and its pressure level. This energy may be recovered using a turbine, for example. Modern passenger car systems have a power class of 70 kW to 100 kW. Accordingly, components and modules are available for this power class. Scaling a fuel cell system for passenger cars or other vehicles to powers of 120 kW to 180 kW, for example, and more [is] presently not known. Furthermore, a plurality of exhaust gas turbochargers or electric turbochargers and/or suppliers for the same, are not available for fuel cell units as they are for other motors such as internal combustion engines.
This entails significant disadvantages for high-powered fuel cell units such as, for example, comparatively large and/or comparatively cost-intensive components, which result in comparatively large and/or comparatively cost-intensive fuel cell systems. Corresponding modules, in particular, turbines and compressors, are presently not available for such fuel cell units and had to be developed from scratch; such a module has low efficiency in a partial load operational range. The fuel cell is therefore not operated at a largely optimal operating point. The modules of the fuel cell unit must be overdimensioned and would operate in their upper load ranges and would be fully utilized only during a fraction of their service life. The response times and/or the dynamics of these modules are also reduced due to their size.
DE 10 2011 114 720 A1 describes a cathode supply for a fuel cell including at least one first air pumping device, the first air pumping device being drivable at least partially by an electric motor, using a voltage level of the fuel cell. Furthermore, the cathode supply includes a second air pumping device, the second air pumping device being connected fluido-mechanically in series to the first air pumping device, and the second air pumping device being drivable by an electrical low-voltage level.
It is an object of the present invention is to scale fuel cell units of fuel cell systems of different power classes, using synergy effects similar to those of presently commercially available components, for internal combustion engines, for example.
Overdimensioning of corresponding new modules to be used and/or already present, in particular, of a turbine and/or a compressor, should be avoided. Furthermore, the fuel cell unit according to the present invention should have a comparatively high efficiency and be able to operate at a largely optimum operating point comparatively often.
The present invention provides a cathode supply for a fuel cell of a fuel cell unit for a fuel cell system, a fuel cell unit for a vehicle, a fuel cell system for a vehicle, and/or a vehicle, in particular, an electrical vehicle.
The cathode supply according to the present invention includes a cathode supply path and a cathode exhaust gas path, at least two fluid pumping devices for pumping a cathode operating medium for the fuel cell being fluido-mechanically coupled into the cathode supply path, and at least one first fluid pumping device of the at least two fluid pumping devices being drivable only on the basis of an enthalpy in a cathode exhaust gas of the fuel cell. The fluid pumping device is used for increasing the fluid pressure of the cathode operating medium and/or for increasing a mass flow rate of the cathode operating medium.
The first fluid pumping device is drivable exclusively fluido-mechanically by the cathode exhaust gas, since the fuel cell has a certain energy content or a certain enthalpy, recoverable according to the present invention, due to its temperature level and its pressure level in the cathode exhaust gas. In some exemplary embodiments, the fluid pumping device is designed as a compressor, a cathode compressor, a pump, etc. The present invention provides a simple scalability of a fuel cell unit or a fuel cell system.
In some exemplary embodiments, at least one second fluid pumping device of the at least two fluid pumping devices is drivable by an electric motor, the second fluid pumping device being drivable exclusively by an electric motor or by the electric motor and additionally by a turbine, in particular, a cathode turbine. This means that the second fluid pumping device is drivable electromechanically and, if necessary, also fluido-mechanically with the aid of an exhaust gas, in particular, of the cathode exhaust gas. In some exemplary embodiments, the cathode supply includes an exhaust gas turbocharger and an electric turbocharger, the exhaust gas turbocharger including the first fluid pumping device and the electric turbocharger including the second fluid pumping device.
In some exemplary embodiments, the first fluid pumping device is designed as a first cathode compressor of the exhaust gas turbocharger, the first cathode compressor being preferably drivable by a cathode turbine of the exhaust gas turbocharger, and the cathode turbine being fluido-mechanically coupled into the cathode exhaust gas path. Here again, the first cathode compressor of the exhaust gas turbocharger is fluido-mechanically coupled into the cathode supply path. The cathode turbine may be designed as a cathode turbine having a variable turbine geometry. Furthermore, the first cathode compressor and the cathode turbine of the exhaust gas turbocharger may also be coupled to each other rotatorily, i.e., mechanically, via a shared shaft or via a transmission.
In some exemplary embodiments, two fluid pumping devices of the at least two fluid pumping devices are connected fluido-mechanically in series or in parallel. For example, if three fluid pumping devices are provided, all three fluid pumping devices are connected in parallel or in series in some exemplary embodiments. In other exemplary embodiments, two of the three fluid pumping devices are connected in parallel, a third fluid pumping device being connected in series to these two fluid pumping devices. Furthermore, in some exemplary embodiments, two of the three fluid pumping devices are connected in series, a third fluid pumping device being connected in parallel to these two fluid pumping devices. Of course, this may be applied similarly to a plurality of fluid pumping devices.
In some exemplary embodiments, the first fluid pumping device is fluido-mechanically coupled into the cathode supply path downstream from an air filter, a wastegate, the second fluid pumping device, a humidifier, and/or a charge air cooler. The first fluid pumping device may be fluido-mechanically coupled into the cathode supply path upstream from the wastegate, the second fluid pumping device, the humidifier, and/or the charge air cooler. In some exemplary embodiments, the cathode turbine is fluido-mechanically coupled into the cathode exhaust gas path upstream or downstream from the humidifier, and/or the wastegate.
In some exemplary embodiments, the second fluid pumping device is coupled into the cathode supply path downstream from the air filter, the wastegate, the first fluid pumping device, the humidifier, and/or the charge air cooler. The second fluid pumping device may be fluido-mechanically coupled into the cathode supply path upstream from the wastegate, the first fluid pumping device, the humidifier, and/or the charge air cooler.
Furthermore, in some exemplary embodiments, the second fluid pumping device is fluido-mechanically coupled into the cathode supply path downstream from the first fluid pumping device, the first fluid pumping device being fluido-mechanically coupled into the cathode supply path preferably upstream and the second fluid pumping device preferably downstream from the humidifier, and the second fluid pumping device being preferably provided upstream from the charge air cooler in particular.
According to other exemplary embodiments, the air filter is fluido-mechanically coupled into the cathode supply path between the first and second fluid pumping device, preferably downstream from the charge air cooler and the wastegate and upstream from the humidifier.
According to the present invention, in some exemplary embodiments a reduction of a component size and/or a module size of system components such as, for example, the humidifier and/or the charge air cooler results, and thus a reduction of a necessary installation space for the fuel cell unit. Furthermore, use of standard components or components already available on the market may result, which saves costs. In addition, use of identical parts results in an increase in the number of applications of the corresponding component and again in cost reduction.
According to the present invention, in some exemplary embodiments an increase in the efficiency of the fuel cell unit results, in particular, in a partial load operational range, due to better layout options of the fuel cell unit, in particular, of the electric turbocharger. A reduction in dynamics of the electric turbocharger is possible and thus a reduction in voltage peaks and/or current peaks in an electrical traction system of the fuel cell system. Accordingly, layout and use of power electronics of the electric turbocharger are also simpler. In addition, increased flexibility results in a fluido-mechanical interconnection of the fuel cell unit.
The present invention is elucidated in greater detail below based on exemplary embodiments, with reference to the appended schematic drawing. Elements and components having an identical, univocal, or similar design and/or function are provided with the same reference numerals in the description of the figures, the list of reference numerals, and/or identified in the figures using the same reference numerals. Possible alternatives to the elucidated exemplary embodiments of the present invention, not elucidated in the description or not illustrated in the drawing, and/or not conclusive alternatives, static or kinetic inversions, combinations, etc. to the explained exemplary embodiments of the present invention or of individual modules, parts or sections thereof, may be derived from the list of reference numerals.
All elucidated features, including those of the list of reference numerals, are applicable not only in the given combination or given combinations, but also in other combinations or by themselves. In particular, it is possible to replace one feature or a plurality of features in the description of the invention, the description of the figures, and/or the list of reference numerals with the aid of the reference numerals and the features assigned thereto. In the figures of the drawing,
The present invention is elucidated in greater detail with the aid of five specific embodiments of a cathode supply 30 for a fuel cell 10 of a fuel cell unit 1 for a vehicle (passenger car, passenger transport vehicle, bus, ATV, motorcycle, utility vehicle, (heavy) truck, construction vehicle, construction machine, special vehicle, rail vehicle). However, the present invention is not limited to the exemplary embodiments described below, but is of a fundamental nature, so that it may be applied to other fuel cell units, for example, of a transport system or of another means of transportation, such as an airplane, or also to transportable or stationary fuel cell units. In
The drawing shows only those sections of fuel cell unit 1 which are needed for understanding the present invention. In particular, an illustration of a periphery of fuel cell unit 1, of sensors, electronic, electrical and power electrical devices and/or systems, etc. is largely omitted. Although the present invention is described in greater detail and illustrated using preferred exemplary embodiments, the present invention is not limited by the provided exemplary embodiments. Other variations may be derived therefrom without departing from the scope of protection of the present invention.
Fuel cell unit 1 includes as one core component fuel cell 10 or a fuel cell stack 10, which preferably has a plurality of individual fuel cells 11, henceforth referred to as individual cells 11, arranged in the form of a stack, and accommodated in a preferably fluid-tight stack housing 16. Each individual cell 11 includes an anode space 12 and a cathode space 13, anode space 12 and cathode space 13 being spatially and electrically separated by a membrane (part of a membrane electrode assembly, see below), preferably of an ion conductive polymer electrolyte membrane (see detail). Fuel cell stack 10 is also simply referred to as fuel cell 10.
Anode spaces 12 and cathode spaces 13 of fuel cell 10 each have, adjacent to the membranes, a catalytic electrode (part of the corresponding membrane electrode assembly 14, see below), i.e., one anode electrode and one cathode electrode, which catalyze a partial reaction of a fuel cell conversion. The anode electrode and the cathode electrode each has a catalytic material, for example, platinum, which is preferably present supported on an electrically conductive supporting material having a comparatively large specific surface, for example, a carbon-based material.
A structure made up of a membrane and associated electrodes is also referred to as membrane electrode assembly 14. A bipolar plate 15 is also situated (in
An anode space 12 is formed between a bipolar plate 15 and an anode electrode of a membrane electrode assembly 14 directly adjacent thereto, and a cathode space 13 of an individual cell 11 (anode space-cathode space pair 12/13) is formed between a cathode electrode of the same membrane electrode assembly 14 and a second bipolar plate 15 directly adjacent thereto. Optionally gas diffusion layers may be situated between membrane electrode assemblies 14 and bipolar plates 15. Membrane electrode assemblies 14 and bipolar plates 15 are thus alternatingly situated or stacked (fuel cell stack 10) in fuel cell 10 or fuel cell stack 10.
For supplying fuel cell 10 or fuel cell stack 10 with operating media 3, 5, fuel cell unit 1 or the fuel cell system has, on the one hand, an anode supply 20 and, on the other hand, a cathode supply 30.
Anode supply 20 includes an anode supply path 21, which is used for feeding an anode operating medium 3 to a fuel 3, for example, hydrogen 3 or a hydrogen-containing gas mixture 3, into anode spaces 12 of fuel cell 10. For this purpose, anode supply path 21 connects a fuel storage 23 or fuel tank 23 to an anode inlet of fuel cell 10. Anode supply 20 further includes an anode exhaust gas path 22, which removes anode exhaust gas 4 from anode spaces 12 through an anode outlet of fuel cell 10. An operating pressure that has built up on an anode side of fuel cell 10 is preferably settable with the aid of a setting means 24 in anode supply path 21.
In addition, anode supply 20 preferably has a fuel recycling line 25, which fluido-mechanically connects anode exhaust gas path 22 to anode supply path 21. Recirculation of anode operating medium 3, i.e., fuel 3 to be actually preferably stored in the tank, is often set up to recycle and use anode operating medium 3 of fuel cell 10 used mostly over-stoichiometrically. Furthermore, a compressor may be provided (not illustrated) in/on fuel recycling line 25. Cathode supply 30 includes a cathode supply path 31, which feeds a cathode operating medium 5, for example, oxygen 5 or an oxygen-containing gas mixture 5, preferably air 5, which may be aspirated from surroundings 2 in particular, to cathode spaces 13 of fuel cell 10. Cathode supply 30 furthermore includes a cathode exhaust gas path 32, which removes a cathode exhaust gas 6, in particular, an exhaust air 6, from cathode spaces 13 of fuel cell 10 and feeds it to an optionally provided exhaust gas device (not illustrated).
For pumping and compressing cathode operating medium 5, at least two fluid pumping devices 33, 133 or air pumping devices 33, 133, are provided or situated in/on cathode supply path 31, i.e., fluido-mechanically coupled into cathode supply path 31. For a primary drive of two fluid pumping devices 33, 133 of the at least two fluid pumping devices 33, 133 different drive principles, in particular, a fluido-mechanical and an electromechanical drive principle, are used. See also
According to the present invention, a first fluid pumping device 133 may be driven exclusively by an energy or enthalpy carried by exhaust gas 6, i.e., exclusively fluido-mechanically. This also means that first fluid pumping device 133 has only one single drive, namely the primary drive. An additional electromechanical (electric motor) or other drive is not expressly provided for first fluid pumping device 133 according to the present invention. In some exemplary embodiments a single fluid pumping device 133 or in some exemplary embodiments, a plurality of or a majority of such first fluid pumping devices 133 are fluido-mechanically coupled into cathode supply path 31.
In some exemplary embodiments first fluid pumping device 133 is designed as a cathode compressor 133 of an exhaust gas turbocharger 100 (only shown in
According to the present invention, a second fluid pumping device 33 may be driven by an electric motor 34, i.e., electromechanically; second fluid pumping device 33 may be driven exclusively by an electric motor (sole drive as primary drive). Electric motor 34 is preferably equipped with power electronics 35. In some exemplary embodiments, second fluid pumping device 33 may be driven, in addition to electromechanical drive 34, also similarly to fluid pumping device 133 by energy or enthalpy in cathode exhaust gas 6, i.e., fluido-mechanically (additional drive as secondary drive). In some exemplary embodiments, a single second fluid pumping device 33 or, in some exemplary embodiments, a plurality of or a majority of such second fluid pumping devices 33 are fluido-mechanically coupled into cathode supply path 31.
In some exemplary embodiments, second fluid pumping device 33 is designed as a cathode compressor 33 of an electric turbocharger 50 (only shown in
According to the specific embodiment illustrated, cathode supply 30 may include a wastegate 37 or a wastegate line 37, which connects cathode supply path 31 or a cathode supply line to cathode exhaust gas path 32 or a cathode exhaust gas line, i.e., represents a cathode-side bypass for fuel cell 10. Wastegate 37 allows an operating pressure of cathode operating medium 5 to be briefly reduced in fuel cell 10, without slowing down the corresponding fluid pumping device 33, 133. A setting means 38 situated in wastegate 37 allows a volume flow rate of cathode operating medium 5 to be set, possibly bypassing fuel cell 10.
All setting means 24, 26, 38 of fuel cell unit 1 may be designed as regulatable, controllable or non-regulatable valves, dampers, throttles, orifices, etc. For insulating fuel cell 10 from surroundings 2, or for any other purpose, at least one additional setting means (not illustrated) may be situated in anode supply 20 and/or cathode supply 30, for example, in/on anode path 21, 22 or a line of anode path 21, 22, and/or in/on a cathode path 31, 32 or a line of cathode path 31, 32.
Fuel cell unit 1 also preferably includes a humidifier 39. Humidifier 39 is, on the one hand, situated in cathode supply path 31 in such a way that cathode operating medium 5 may flow through it. On the other hand, humidifier 39 is preferably situated in cathode exhaust gas path 32 in such a way that cathode exhaust gas 6 may flow through it. Humidifier 39 is situated in cathode supply path 31 preferably between first fluid pumping device 133 or second fluid pumping device 33 (see again
Different further details of the fuel cell system or fuel cell unit 1 or fuel cell 10/fuel cell stack 10, of anode supply 20 and/or cathode supply 30 are not illustrated in
Furthermore, a water separator may be installed in anode exhaust gas path 22 and/or in cathode exhaust gas path 32, with the aid of which a product water emerging from the corresponding partial reaction of fuel cell 10 may be condensed and/or separated, and possibly removed into a water collector for storage. Furthermore, anode supply 20 may alternatively or additionally have a humidifier 39 similar to that of cathode supply 30. Furthermore, anode exhaust gas path 22 may open into cathode exhaust gas path 32 or vice-versa; anode exhaust gas 4 and cathode exhaust gas 6 may possibly be removed via the shared exhaust gas system. In addition, in some exemplary embodiments, cathode operating medium 5 may flow through a charge air cooler 40 (see
In order to compensate for the disadvantage that, in the case where a majority of or a plurality of fluid pumping devices are used for cathode operating medium 5, and the plurality of or a majority of fluid pumping devices may be driven by electric motors, at least one of these fluid pumping devices referred to above and henceforth referred to as first fluid pumping device 133, is designed in such a way that it is drivable, as explained above, exclusively using energy recoverable from cathode exhaust gas 6. This first fluid pumping device 133 thus needs no additional electromotive drive, i.e., no electric power, for example, from fuel cell unit 1.
This first fluid pumping device 133 may be used at different points of fuel cell unit 1. Thus, first fluid pumping device 133 may be fluido-mechanically coupled into cathode supply path 31, for example, upstream from humidifier 39 and charge air cooler 40 (see
In the first specific embodiment shown in
The second specific embodiment shown in
In the preferred fourth specific embodiment shown in
Of course, other exemplary embodiments are also feasible; for example, a majority of exhaust gas turbochargers and/or a majority of electric turbochargers may be used. In some exemplary embodiments, an additional exhaust gas turbocharger is designed as above-described exhaust gas turbocharger 100. Furthermore, in some exemplary embodiments, another electric turbocharger is designed as above-described electric turbocharger 50. Furthermore, for example, charge air cooler 40 is omitted in some specific embodiments. In addition, another position of wastegate 37 or an opening of wastegate 37 in/on cathode supply path 31 and/or in/on cathode exhaust gas path 32 is possible.
According to the present invention, two or a plurality of fluid pumping devices 33, 133 connected in parallel or in series are used for cathode operating medium 5. At least one of fluid pumping devices 33, 133 here identified as first fluid pumping device 133, may be driven only by the enthalpy in cathode exhaust gas 6 of fuel cell 10. This is accomplished, for example, with the aid of exhaust gas turbocharger 100, which includes first fluid pumping device 133, in some exemplary embodiments a majority of such exhaust gas turbochargers 100 being provided in fuel cell unit 1. Electric turbocharger 50 is preferably connected to exhaust gas turbocharger 100 in series (see
Lucas, Christian, Brinkmeier, Jan-Philipp, Scholz, Hannes, Grundei, Daniel, Schlitzberger, Christian
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| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| Nov 03 2016 | Volkswagen AG | (assignment on the face of the patent) | / | |||
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| Nov 03 2016 | LUCAS, CHRISTIAN | Volkswagen AG | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 040329 | /0537 | |
| Nov 03 2016 | SCHOLZ, HANNES | Volkswagen AG | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 040329 | /0537 | |
| Nov 03 2016 | BRINKMEIER, JAN-PHILIPP | Volkswagen AG | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 040329 | /0537 | |
| Nov 08 2016 | SCHLITZBERGER, CHRISTIAN | Volkswagen AG | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 040329 | /0537 | |
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